Mixture of p-Xylene + Tetrahydrofuran

Excel

p-Xylene

Name
p-Xylene
InChI
InChI=1S/C8H10/c1-7-3-5-8(2)6-4-7/h3-6H,1-2H3
InChI Key
URLKBWYHVLBVBO-UHFFFAOYSA-N
Formula
C8H10
SMILES
Cc1ccc(C)cc1
Mol. Weight (g/mol)
106.17
CAS
106-42-3

Tetrahydrofuran

Name
Tetrahydrofuran
InChI
InChI=1S/C4H8O/c1-2-4-5-3-1/h1-4H2
InChI Key
WYURNTSHIVDZCO-UHFFFAOYSA-N
Formula
C4H8O
SMILES
C1CCOC1
Mol. Weight (g/mol)
72.11
CAS
109-99-9
Cheméo is a service of Céondo GmbH, since 2007, we provide simulation, modelling and software development services for the industry. Do not hesitate to contact us for your projects.

Datasets

  1. η - Viscosity, Pa*s (2)
  2. n0 - Refractive index (Na D-line) (2)
  3. csound,fluid - Speed of Sound, m/s (2)
  4. Vapor Liquid Equilibrium at Constant Pressure

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Tetrahydrofuran (2) - Liquid Viscosity, Pa*s - Liquid
288.15 0.0000 0.0007
288.15 0.0840 0.0007
288.15 0.1716 0.0007
288.15 0.2322 0.0007
288.15 0.2934 0.0007
288.15 0.3548 0.0007
288.15 0.4284 0.0006
288.15 0.4896 0.0006
288.15 0.5518 0.0006
288.15 0.6201 0.0006
288.15 0.6825 0.0006
288.15 0.7414 0.0006
288.15 0.8102 0.0006
288.15 0.8756 0.0005
288.15 0.9409 0.0005
288.15 1.0000 0.0005
298.15 0.0000 0.0006
298.15 0.0840 0.0006
298.15 0.1716 0.0006
298.15 0.2322 0.0006
298.15 0.2934 0.0006
298.15 0.3548 0.0006
298.15 0.4284 0.0006
298.15 0.4896 0.0006
298.15 0.5518 0.0005
298.15 0.6201 0.0005
298.15 0.6825 0.0005
298.15 0.7414 0.0005
298.15 0.8102 0.0005
298.15 0.8756 0.0005
298.15 0.9409 0.0005
298.15 1.0000 0.0005
308.15 0.0000 0.0006
308.15 0.0840 0.0005
308.15 0.1716 0.0005
308.15 0.2322 0.0005
308.15 0.2934 0.0005
308.15 0.3548 0.0005
308.15 0.4284 0.0005
308.15 0.4896 0.0005
308.15 0.5518 0.0005
308.15 0.6201 0.0005
308.15 0.6825 0.0005
308.15 0.7414 0.0005
308.15 0.8102 0.0005
308.15 0.8756 0.0004
308.15 0.9409 0.0004
308.15 1.0000 0.0004
318.15 0.0000 0.0005
318.15 0.0840 0.0005
318.15 0.1716 0.0005
318.15 0.2322 0.0005
318.15 0.2934 0.0005
318.15 0.3548 0.0005
318.15 0.4284 0.0005
318.15 0.4896 0.0005
318.15 0.5518 0.0005
318.15 0.6201 0.0004
318.15 0.6825 0.0004
318.15 0.7414 0.0004
318.15 0.8102 0.0004
318.15 0.8756 0.0004
318.15 0.9409 0.0004
318.15 1.0000 0.0004

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Tetrahydrofuran (2) - Liquid Viscosity, Pa*s - Liquid
288.15 0.0000 0.0007
288.15 0.0840 0.0007
288.15 0.1716 0.0007
288.15 0.2322 0.0007
288.15 0.2934 0.0007
288.15 0.3548 0.0007
288.15 0.4284 0.0006
288.15 0.4896 0.0006
288.15 0.5518 0.0006
288.15 0.6201 0.0006
288.15 0.6825 0.0006
288.15 0.7414 0.0006
288.15 0.8102 0.0006
288.15 0.8756 0.0005
288.15 0.9409 0.0005
288.15 1.0000 0.0005
298.15 0.0000 0.0006
298.15 0.0840 0.0006
298.15 0.1716 0.0006
298.15 0.2322 0.0006
298.15 0.2934 0.0006
298.15 0.3548 0.0006
298.15 0.4284 0.0006
298.15 0.4896 0.0006
298.15 0.5518 0.0005
298.15 0.6201 0.0005
298.15 0.6825 0.0005
298.15 0.7414 0.0005
298.15 0.8102 0.0005
298.15 0.8756 0.0005
298.15 0.9409 0.0005
298.15 1.0000 0.0005
308.15 0.0000 0.0006
308.15 0.0840 0.0005
308.15 0.1716 0.0005
308.15 0.2322 0.0005
308.15 0.2934 0.0005
308.15 0.3548 0.0005
308.15 0.4284 0.0005
308.15 0.4896 0.0005
308.15 0.5518 0.0005
308.15 0.6201 0.0005
308.15 0.6825 0.0005
308.15 0.7414 0.0005
308.15 0.8102 0.0005
308.15 0.8756 0.0004
308.15 0.9409 0.0004
308.15 1.0000 0.0004
318.15 0.0000 0.0005
318.15 0.0840 0.0005
318.15 0.1716 0.0005
318.15 0.2322 0.0005
318.15 0.2934 0.0005
318.15 0.3548 0.0005
318.15 0.4284 0.0005
318.15 0.4896 0.0005
318.15 0.5518 0.0005
318.15 0.6201 0.0004
318.15 0.6825 0.0004
318.15 0.7414 0.0004
318.15 0.8102 0.0004
318.15 0.8756 0.0004
318.15 0.9409 0.0004
318.15 1.0000 0.0004

Refractive index (Na D-line) [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Tetrahydrofuran (2) - Liquid Refractive index (Na D-line) - Liquid
288.15 0.0000 1.4985
288.15 0.0840 1.4936
288.15 0.1716 1.4881
288.15 0.2322 1.4842
288.15 0.2934 1.48
288.15 0.3548 1.4755
288.15 0.4284 1.4698
288.15 0.4896 1.4648
288.15 0.5518 1.4594
288.15 0.6201 1.4531
288.15 0.6825 1.447
288.15 0.7414 1.4409
288.15 0.8102 1.4333
288.15 0.8756 1.4256
288.15 0.9409 1.4174
288.15 1.0000 1.4094
293.15 0.0000 1.4959
293.15 0.0840 1.491
293.15 0.1716 1.4855
293.15 0.2322 1.4816
293.15 0.2934 1.4774
293.15 0.3548 1.4729
293.15 0.4284 1.4672
293.15 0.4896 1.4622
293.15 0.5518 1.4568
293.15 0.6201 1.4505
293.15 0.6825 1.4444
293.15 0.7414 1.4383
293.15 0.8102 1.4308
293.15 0.8756 1.4231
293.15 0.9409 1.4149
293.15 1.0000 1.407
298.15 0.0000 1.4933
298.15 0.0840 1.4884
298.15 0.1716 1.4829
298.15 0.2322 1.479
298.15 0.2934 1.4748
298.15 0.3548 1.4703
298.15 0.4284 1.4646
298.15 0.4896 1.4596
298.15 0.5518 1.4542
298.15 0.6201 1.448
298.15 0.6825 1.4419
298.15 0.7414 1.4358
298.15 0.8102 1.4282
298.15 0.8756 1.4206
298.15 0.9409 1.4125
298.15 1.0000 1.4046
303.15 0.0000 1.4907
303.15 0.0840 1.4858
303.15 0.1716 1.4803
303.15 0.2322 1.4764
303.15 0.2934 1.4722
303.15 0.3548 1.4677
303.15 0.4284 1.4621
303.15 0.4896 1.4571
303.15 0.5518 1.4517
303.15 0.6201 1.4454
303.15 0.6825 1.4394
303.15 0.7414 1.4333
303.15 0.8102 1.4258
303.15 0.8756 1.4182
303.15 0.9409 1.4101
303.15 1.0000 1.4023
308.15 0.0000 1.4881
308.15 0.0840 1.4832
308.15 0.1716 1.4777
308.15 0.2322 1.4738
308.15 0.2934 1.4696
308.15 0.3548 1.4651
308.15 0.4284 1.4595
308.15 0.4896 1.4545
308.15 0.5518 1.4491
308.15 0.6201 1.4429
308.15 0.6825 1.4368
308.15 0.7414 1.4308
308.15 0.8102 1.4233
308.15 0.8756 1.4157
308.15 0.9409 1.4077
308.15 1.0000 1.3999
313.15 0.0000 1.4855
313.15 0.0840 1.4806
313.15 0.1716 1.4751
313.15 0.2322 1.4712
313.15 0.2934 1.467
313.15 0.3548 1.4625
313.15 0.4284 1.4569
313.15 0.4896 1.4519
313.15 0.5518 1.4465
313.15 0.6201 1.4403
313.15 0.6825 1.4342
313.15 0.7414 1.4282
313.15 0.8102 1.4207
313.15 0.8756 1.4132
313.15 0.9409 1.4052
313.15 1.0000 1.3975
318.15 0.0000 1.483
318.15 0.0840 1.478
318.15 0.1716 1.4726
318.15 0.2322 1.4686
318.15 0.2934 1.4644
318.15 0.3548 1.46
318.15 0.4284 1.4544
318.15 0.4896 1.4494
318.15 0.5518 1.4441
318.15 0.6201 1.4378
318.15 0.6825 1.4318
318.15 0.7414 1.4258
318.15 0.8102 1.4183
318.15 0.8756 1.4108
318.15 0.9409 1.4028
318.15 1.0000 1.3951

Refractive index (Na D-line) [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Tetrahydrofuran (2) - Liquid Refractive index (Na D-line) - Liquid
288.15 0.0000 1.4985
288.15 0.0840 1.4936
288.15 0.1716 1.4881
288.15 0.2322 1.4842
288.15 0.2934 1.48
288.15 0.3548 1.4755
288.15 0.4284 1.4698
288.15 0.4896 1.4648
288.15 0.5518 1.4594
288.15 0.6201 1.4531
288.15 0.6825 1.447
288.15 0.7414 1.4409
288.15 0.8102 1.4333
288.15 0.8756 1.4256
288.15 0.9409 1.4174
288.15 1.0000 1.4094
293.15 0.0000 1.4959
293.15 0.0840 1.491
293.15 0.1716 1.4855
293.15 0.2322 1.4816
293.15 0.2934 1.4774
293.15 0.3548 1.4729
293.15 0.4284 1.4672
293.15 0.4896 1.4622
293.15 0.5518 1.4568
293.15 0.6201 1.4505
293.15 0.6825 1.4444
293.15 0.7414 1.4383
293.15 0.8102 1.4308
293.15 0.8756 1.4231
293.15 0.9409 1.4149
293.15 1.0000 1.407
298.15 0.0000 1.4933
298.15 0.0840 1.4884
298.15 0.1716 1.4829
298.15 0.2322 1.479
298.15 0.2934 1.4748
298.15 0.3548 1.4703
298.15 0.4284 1.4646
298.15 0.4896 1.4596
298.15 0.5518 1.4542
298.15 0.6201 1.448
298.15 0.6825 1.4419
298.15 0.7414 1.4358
298.15 0.8102 1.4282
298.15 0.8756 1.4206
298.15 0.9409 1.4125
298.15 1.0000 1.4046
303.15 0.0000 1.4907
303.15 0.0840 1.4858
303.15 0.1716 1.4803
303.15 0.2322 1.4764
303.15 0.2934 1.4722
303.15 0.3548 1.4677
303.15 0.4284 1.4621
303.15 0.4896 1.4571
303.15 0.5518 1.4517
303.15 0.6201 1.4454
303.15 0.6825 1.4394
303.15 0.7414 1.4333
303.15 0.8102 1.4258
303.15 0.8756 1.4182
303.15 0.9409 1.4101
303.15 1.0000 1.4023
308.15 0.0000 1.4881
308.15 0.0840 1.4832
308.15 0.1716 1.4777
308.15 0.2322 1.4738
308.15 0.2934 1.4696
308.15 0.3548 1.4651
308.15 0.4284 1.4595
308.15 0.4896 1.4545
308.15 0.5518 1.4491
308.15 0.6201 1.4429
308.15 0.6825 1.4368
308.15 0.7414 1.4308
308.15 0.8102 1.4233
308.15 0.8756 1.4157
308.15 0.9409 1.4077
308.15 1.0000 1.3999
313.15 0.0000 1.4855
313.15 0.0840 1.4806
313.15 0.1716 1.4751
313.15 0.2322 1.4712
313.15 0.2934 1.467
313.15 0.3548 1.4625
313.15 0.4284 1.4569
313.15 0.4896 1.4519
313.15 0.5518 1.4465
313.15 0.6201 1.4403
313.15 0.6825 1.4342
313.15 0.7414 1.4282
313.15 0.8102 1.4207
313.15 0.8756 1.4132
313.15 0.9409 1.4052
313.15 1.0000 1.3975
318.15 0.0000 1.483
318.15 0.0840 1.478
318.15 0.1716 1.4726
318.15 0.2322 1.4686
318.15 0.2934 1.4644
318.15 0.3548 1.46
318.15 0.4284 1.4544
318.15 0.4896 1.4494
318.15 0.5518 1.4441
318.15 0.6201 1.4378
318.15 0.6825 1.4318
318.15 0.7414 1.4258
318.15 0.8102 1.4183
318.15 0.8756 1.4108
318.15 0.9409 1.4028
318.15 1.0000 1.3951

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Tetrahydrofuran (2) - Liquid Speed of sound, m/s - Liquid
288.15 0.0000 1357.5
288.15 0.0840 1356.0
288.15 0.1716 1354.2
288.15 0.2322 1353.1
288.15 0.2934 1351.7
288.15 0.3548 1350.2
288.15 0.4284 1348.1
288.15 0.4896 1346.2
288.15 0.5518 1344.1
288.15 0.6201 1341.5
288.15 0.6825 1338.9
288.15 0.7414 1336.3
288.15 0.8102 1333.1
288.15 0.8756 1329.8
288.15 0.9409 1326.4
288.15 1.0000 1323.1
298.15 0.0000 1316.4
298.15 0.0840 1314.1
298.15 0.1716 1311.7
298.15 0.2322 1310.1
298.15 0.2934 1308.3
298.15 0.3548 1306.5
298.15 0.4284 1304.0
298.15 0.4896 1301.8
298.15 0.5518 1299.4
298.15 0.6201 1296.6
298.15 0.6825 1293.7
298.15 0.7414 1290.9
298.15 0.8102 1287.6
298.15 0.8756 1284.3
298.15 0.9409 1280.8
298.15 1.0000 1277.6
308.15 0.0000 1268.0
308.15 0.0840 1265.7
308.15 0.1716 1263.2
308.15 0.2322 1261.6
308.15 0.2934 1259.9
308.15 0.3548 1258.1
308.15 0.4284 1255.7
308.15 0.4896 1253.7
308.15 0.5518 1251.5
308.15 0.6201 1248.8
308.15 0.6825 1246.2
308.15 0.7414 1243.6
308.15 0.8102 1240.6
308.15 0.8756 1237.5
308.15 0.9409 1234.4
308.15 1.0000 1231.5
318.15 0.0000 1230.3
318.15 0.0840 1227.2
318.15 0.1716 1224.0
318.15 0.2322 1221.9
318.15 0.2934 1219.6
318.15 0.3548 1217.3
318.15 0.4284 1214.5
318.15 0.4896 1212.0
318.15 0.5518 1209.3
318.15 0.6201 1206.2
318.15 0.6825 1203.3
318.15 0.7414 1200.4
318.15 0.8102 1197.0
318.15 0.8756 1193.7
318.15 0.9409 1190.4
318.15 1.0000 1187.2

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Tetrahydrofuran (2) - Liquid Speed of sound, m/s - Liquid
288.15 0.0000 1357.5
288.15 0.0840 1356.0
288.15 0.1716 1354.2
288.15 0.2322 1353.1
288.15 0.2934 1351.7
288.15 0.3548 1350.2
288.15 0.4284 1348.1
288.15 0.4896 1346.2
288.15 0.5518 1344.1
288.15 0.6201 1341.5
288.15 0.6825 1338.9
288.15 0.7414 1336.3
288.15 0.8102 1333.1
288.15 0.8756 1329.8
288.15 0.9409 1326.4
288.15 1.0000 1323.1
298.15 0.0000 1316.4
298.15 0.0840 1314.1
298.15 0.1716 1311.7
298.15 0.2322 1310.1
298.15 0.2934 1308.3
298.15 0.3548 1306.5
298.15 0.4284 1304.0
298.15 0.4896 1301.8
298.15 0.5518 1299.4
298.15 0.6201 1296.6
298.15 0.6825 1293.7
298.15 0.7414 1290.9
298.15 0.8102 1287.6
298.15 0.8756 1284.3
298.15 0.9409 1280.8
298.15 1.0000 1277.6
308.15 0.0000 1268.0
308.15 0.0840 1265.7
308.15 0.1716 1263.2
308.15 0.2322 1261.6
308.15 0.2934 1259.9
308.15 0.3548 1258.1
308.15 0.4284 1255.7
308.15 0.4896 1253.7
308.15 0.5518 1251.5
308.15 0.6201 1248.8
308.15 0.6825 1246.2
308.15 0.7414 1243.6
308.15 0.8102 1240.6
308.15 0.8756 1237.5
308.15 0.9409 1234.4
308.15 1.0000 1231.5
318.15 0.0000 1230.3
318.15 0.0840 1227.2
318.15 0.1716 1224.0
318.15 0.2322 1221.9
318.15 0.2934 1219.6
318.15 0.3548 1217.3
318.15 0.4284 1214.5
318.15 0.4896 1212.0
318.15 0.5518 1209.3
318.15 0.6201 1206.2
318.15 0.6825 1203.3
318.15 0.7414 1200.4
318.15 0.8102 1197.0
318.15 0.8756 1193.7
318.15 0.9409 1190.4
318.15 1.0000 1187.2

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 95.8 (VLE)

T [K] - VLE x1[mol/mol] of Tetrahydrofuran (2) - Liquid
409.35 0.0000
385.15 0.1855
373.05 0.3130
362.65 0.4511
351.75 0.6279
345.35 0.7523
338.55 0.9101
335.55 1.0000

Sources